Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
  • C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
  • C08G65/32—Polymers modified by chemical after-treatment
  • C08G65/321—Polymers modified by chemical after-treatment with inorganic compounds
  • C08G65/324—Polymers modified by chemical after-treatment with inorganic compounds containing oxygen
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
  • C08G65/002—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from unsaturated compounds
  • C08G65/005—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from unsaturated compounds containing halogens
  • C08G65/007—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from unsaturated compounds containing halogens containing fluorine

Definitions

• the invention relates to a process for the preparation of perfluoropolyoxyalkylenes functionalized with hydroxyl end groups.
• Said process has a higher productivity since in the reduction reaction a lower amount of reducing agent is used. Further a lower hydrogen development is noticed during the reaction. This makes the process better controllable from the industrial safety point of view and economically cheaper.
• Monofunctional and bifunctional perfluoropolyoxyalkylenes having hydroxyl end groups of the -CH 2 OH type are known in the prior art.
• the perfluoropolyethers with hydroxyl end groups can be prepared by reduction of the corresponding ester precursors, i.e. starting from perfluoropolyethers having one or two end groups -COOR wherein R is a linear or branched C1-C5 alkyl. Said process is described for example in the patents GB 1,309,401, USP 3,847,978.
• the reduction reaction is carried out by using reducing agents in inert solvents.
• metal hydrides such as for example lithium-aluminum hydride (LiAlH 4 ), dissolved in inert solvents such as tetrahydrofuran, diglyme or dioxane can be mentioned; preferably as reducing agent sodium-boron hydride (NaBH 4 ) in the above mentioned inert solvents or in protic solvents such as methanol, ethanol, is used.
• the process can be schematized with the following reactions, by using sodium-boron hydride as reducing agent and a bifunctional ester with both end groups -COOC 2 H 5 as precursor:
• the Applicant has surprisingly and unexpectedly found that the reduction reaction to obtain perfluoropolyethers having hydroxyl -CH 2 OH end groups, starting from the corresponding ester precursors, can be advantageously carried out by adding in the reaction mixture besides the reducing agent, an organic base. It has been unexpectedly found that the presence of this organic base allows to carry out the reducing reaction by using a small excess of the reducing agent with respect to the stoichiometric amount, generally lower than 15%, and surprisingly that it inhibits the hydrogen development during the process.
• the organic bases used in the process of the present invention are selected from alcoholates and thioalcoholates of alkaline or alkaline-earth metals, having alkyl, cycloaliphatic, aromatic chain or combinations thereof; or nitrogenous bases which do not give condensation reactions with the fluorinated ester, such as for example amidation reactions.
• the following bases are preferably used: sodium or potassium alcoholates such as for example potassium terbutylate or sodium ethylate, more preferably sodium ethylate; in the class of the nitrogenous bases, alkyl, cycloalipahtic and aromatic tertiary amines, such as for example triethylamine, diazabicyclo-octane (DABCO), pyridine, can be mentioned. Also a mixture of the above mentioned organic bases can be used.
• the class of the above mentioned alcoholates is used.
• solvents of the reaction inert solvents such as for example, tetrahydrofuran, diglyme, dioxane or protic solvents such as for example methanol, ethanol, isopropanol, isobutanol or mixtures thereof, preferably ethanol, etc.
• solvents of the reaction inert solvents such as for example, tetrahydrofuran, diglyme, dioxane or protic solvents such as for example methanol, ethanol, isopropanol, isobutanol or mixtures thereof, preferably ethanol, etc.
• mixtures of inert solvents and protic solvents can be used.
• metal hydrides such as for example lithium-aluminum hydride (LiAlH 4 ), sodium-boron hydride (NaBH 4 ), lithium-boron hydride, etc., dissolved in the above mentioned reaction solvents, can be used.
• metal hydrides such as for example lithium-aluminum hydride (LiAlH 4 ), sodium-boron hydride (NaBH 4 ), lithium-boron hydride, etc., dissolved in the above mentioned reaction solvents, can be used.
• sodium-boron hydride is used as sodium-boron hydride.
• R f preferably comprises the following repeating units statistically distributed along the polymer chain:
• reaction for obtaining the invention compounds of formula (I) is preferably carried out at temperatures comprised between 0°C and the boiling temperature of the solvent, preferably between 0°C and 30°C.
• the reducing agent preferably sodium-boron hydride, is used, in an amount in the range 0.1-15% by weight based on the solvent weight.
• the used base amount can range between 0.1 and 100% by moles with respect to the reducing agent, preferably between 2 and 15% by moles, still more preferably between 5 and 15% by moles.
• the reducing agent excess, preferably sodium-boron hydride, necessary for reducing the ester, is in the range 0-30% with respect to the stoichiometric value, preferably 10-20%.
• step b) The product hydrolysis and isolation step (step b) is carried out according to known methods in the prior art. Generally hydrolysis is carried out by slowly adding the reaction product obtained in step a) to an aqueous HCl solution, preferably at a 5-10% concentration by weight, in an equiponderal amount with respect to the initially fed ester. The addition of the products of step a) to the acid solution is carried out gradually due to the hydrogen development deriving from the hydrolysis of the possible excess of the unreacted reducing agent. Alternatively, the hydrolysis step can be carried out by using water in a ratio by weight 2:1 with respect to the initially fed ester. Further aqueous washings can be optionally made at the end of step b) to completely eliminate the inorganic salts from the reduced fluorinated product.
• the hydrolysis of the reaction products of step a) can be also carried by directly feeding the hydrolyzing solution or the water of step b) in the reaction mixture of step a).
• a 3 l jacketed reactor equipped with mechanical stirrer and directly connected to a volumetric gas reader, is charged with ethanol (770 g), sodium ethoxylate (10 g, 0.147 moles) and NaBH 4 (56 g, 1.47 moles). The reaction mixture is then heated to 10°C, maintaining the temperature in external jacket at 8°C.
• ethanol 400 g
• potassium ter-butylate 6 g, 0.05 moles
• NaBH 4 32 g, 0.84 moles
• ethanol 102 g
• sodium ethylate 1.5 g, 0.022 moles
• NaBH 4 8.5 g, 0.23 moles

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• Chemical & Material Sciences (AREA)
• Health & Medical Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• Inorganic Chemistry (AREA)
• General Chemical & Material Sciences (AREA)
• Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
• Polyethers (AREA)
• Lubricants (AREA)
• Fire-Extinguishing Compositions (AREA)

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• 2000
  • 2000-01-04 IT IT2000MI000003A patent/IT1317716B1/it active
  • 2000-12-21 EP EP20000128069 patent/EP1114842B1/de not_active Expired - Lifetime
  • 2000-12-21 DE DE60012127T patent/DE60012127T2/de not_active Expired - Fee Related
  • 2000-12-26 JP JP2000395026A patent/JP2001226482A/ja not_active Withdrawn
  • 2000-12-29 US US09/750,101 patent/US6509509B2/en not_active Expired - Fee Related

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